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JP6913454B2 - How to purify volatile organochlorine compounds - Google Patents
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JP6913454B2 - How to purify volatile organochlorine compounds - Google Patents

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JP6913454B2
JP6913454B2 JP2016232127A JP2016232127A JP6913454B2 JP 6913454 B2 JP6913454 B2 JP 6913454B2 JP 2016232127 A JP2016232127 A JP 2016232127A JP 2016232127 A JP2016232127 A JP 2016232127A JP 6913454 B2 JP6913454 B2 JP 6913454B2
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陽 高畑
陽 高畑
雅子 伊藤
雅子 伊藤
亮哉 渡邉
亮哉 渡邉
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本発明は、揮発性有機塩素化合物を浄化する方法に関する。特に、本発明は、ロドコッカス(Rhodococcus)属の細菌を用いて過酸化水素の存在下で揮発性有機塩素化合物を浄化する方法に関する。 The present invention relates to a method for purifying volatile organochlorine compounds. In particular, the present invention relates to a method of purifying volatile organochlorine compounds in the presence of hydrogen peroxide using bacteria of the genus Rhodococcus.

微生物を用いる浄化技術は、廃水処理における活性汚泥法、嫌気処理法等に広く利用されている。また、近年では、有害化学物質に汚染された土壌及び地下水を微生物によって浄化する技術(バイオレメディエーション)が、環境負荷及び浄化コストの小さい方法として注目されている。 Purification techniques using microorganisms are widely used in activated sludge methods, anaerobic treatment methods, etc. in wastewater treatment. Further, in recent years, a technique (bioremediation) for purifying soil and groundwater contaminated with harmful chemical substances by microorganisms has been attracting attention as a method having a small environmental load and purification cost.

例えば、嫌気性細菌を利用した浄化技術が報告されている。具体的には、トリクロロエチレン、シス-1,2-ジクロロエチレン等の塩素化エチレン類で汚染された地下水を浄化するために、微生物の栄養源となる有機物を浄化井戸等から帯水層中に注入し、地下水を嫌気環境にし、嫌気性脱塩素化細菌を活性化させて、塩素化エチレンを無害なエチレンに浄化する技術が広く実用化されている(非特許文献1)。しかしながら、この技術では、脱塩素化細菌が塩素化エチレンの塩素を一個ずつ水素に置換するため、浄化過程において塩化ビニルモノマーが中間生成物として必ず生成する(図1)。塩化ビニルモノマーは、環境省により2009年に地下水環境基準の項目に追加されている。塩化ビニルモノマーの規制濃度はトリクロロエチレン及びシス-1,2-ジクロロエチレンと比較して1オーダー以上小さいことから、浄化の進捗状況によっては地下水中に環境基準値を大幅に超過する塩化ビニルモノマーが生成し、二次的な地下水汚染が生じるおそれがある。 For example, purification techniques using anaerobic bacteria have been reported. Specifically, in order to purify groundwater contaminated with chlorinated ethylenes such as trichlorethylene and cis-1,2-dichloroethylene, organic substances that serve as nutrient sources for bacteria are injected into the aquifer from purification wells and the like. , A technique of making groundwater into an anaerobic environment, activating anaerobic dechlorinating bacteria, and purifying chlorinated ethylene into harmless ethylene has been widely put into practical use (Non-Patent Document 1). However, in this technique, dechlorinating bacteria replace chlorine in chlorinated ethylene one by one with hydrogen, so that vinyl chloride monomer is always produced as an intermediate product in the purification process (Fig. 1). Vinyl chloride monomer was added to the groundwater environmental standard item in 2009 by the Ministry of the Environment. Since the regulated concentration of vinyl chloride monomer is one order smaller than that of trichlorethylene and cis-1,2-dichloroethylene, vinyl chloride monomer that greatly exceeds the environmental standard value may be generated in groundwater depending on the progress of purification. , Secondary groundwater pollution may occur.

嫌気性細菌を利用した浄化技術に加えて、好気性細菌を利用した浄化技術も報告されている。好気性細菌として、トリクロロエチレン、シス-1,2-ジクロロエチレン等を分解可能な好気性細菌の存在が多く報告されている。好気的な脱塩素化反応は、トルエン、フェノール、メタン等を単一炭素源として増殖するトルエン資化性菌、フェノール資化性菌、メタン資化性菌等によって主に行われる。これらの菌が、トルエン、フェノール、メタン等を好気条件下で炭素源として利用する際に生成する酸化酵素は、基質特異性が広い。例えば、メタンオキシゲナーゼの場合、メタンと共にトリクロロエチレンが存在していると、メタンの酸化に加えて、トリクロロエチレンの共代謝(共酸化)反応が同時に進行して、トリクロロエチレンの脱塩素化反応が促進することが知られている。しかしながら、これらの共代謝反応を促進するために必要な炭素源(電子供与体)は、トルエン、フェノール等の有害な物質であったり、メタン等の水に溶解しにくい物質であったりするため、地下環境への炭素源の有効な供給手段が存在しないことが課題となっていた。 In addition to purification technology using anaerobic bacteria, purification technology using aerobic bacteria has also been reported. As aerobic bacteria, the existence of aerobic bacteria capable of decomposing trichlorethylene, cis-1,2-dichloroethylene and the like has been widely reported. The aerobic dechlorination reaction is mainly carried out by toluene-utilizing bacteria, phenol-utilizing bacteria, methane-utilizing bacteria and the like that grow using toluene, phenol, methane or the like as a single carbon source. The oxidase produced by these bacteria when using toluene, phenol, methane, etc. as a carbon source under aerobic conditions has a wide substrate specificity. For example, in the case of methane oxygenase, when trichlorethylene is present together with methane, the co-metabolization (cooxidation) reaction of trichlorethylene proceeds at the same time in addition to the oxidation of methane, and the dechlorination reaction of trichlorethylene is promoted. Are known. However, the carbon source (electron donor) required to promote these co-metabolism reactions is a harmful substance such as toluene or phenol, or a substance that is difficult to dissolve in water such as methane. The problem was that there was no effective means of supplying carbon sources to the underground environment.

なお、炭素源を必要としない細菌を利用した浄化技術も報告されている(特許文献1)。特許文献1は、炭素源を必要としない細菌(JMP1000株)、及び過酸化水素水から供給される酸素を用いた浄化技術を開示している。JMP1000株は1,000 ppm(0.1%)の過酸化水素水に対して耐性を有することが開示されている。具体的には、特許文献1は、バイアル瓶に1,000 ppmの過酸化水素を含む培地、及びJMP1000株の菌懸濁液(菌体濃度:3.1×107 cfu/ml)1 mlを添加し、完全密封した後、トリクロロエチレン及びトランス-1,2-ジクロロエチレンを液中濃度が10 ppm(10 mg/l)となるようにガスタイトシリンジで添加し、20℃で80時間振盪培養した結果、トリクロロエチレンが59%分解し、トランス-1,2-ジクロロエチレンが71%分解したことを開示している。JMP1000株の分解能は十分ではなく、4日程度ではトリクロロエチレン及びトランス-1,2-ジクロロエチレンを完全に分解することはできない。なお、特許文献1は、JMP1000株によるシス-1,2-ジクロロエチレンの分解について開示していない。 A purification technique using bacteria that does not require a carbon source has also been reported (Patent Document 1). Patent Document 1 discloses a purification technique using a bacterium (JMP1000 strain) that does not require a carbon source and oxygen supplied from a hydrogen peroxide solution. The JMP1000 strain is disclosed to be resistant to 1,000 ppm (0.1%) hydrogen peroxide solution. Specifically, in Patent Document 1, a medium containing 1,000 ppm of hydrogen peroxide and 1 ml of a bacterial suspension of JMP1000 strain (cell concentration: 3.1 × 10 7 cfu / ml) were added to a vial. After completely sealing, trichloroethylene and trans-1,2-dichloroethylene were added with a gas tight syringe so that the concentration in the liquid was 10 ppm (10 mg / l), and the mixture was shake-cultured at 20 ° C. for 80 hours. It is disclosed that 59% decomposition was carried out and trans-1,2-dichloroethylene was decomposed by 71%. The resolution of the JMP1000 strain is not sufficient, and trichlorethylene and trans-1,2-dichloroethylene cannot be completely decomposed in about 4 days. Patent Document 1 does not disclose the decomposition of cis-1,2-dichloroethylene by the JMP1000 strain.

特開平10-295366号公報Japanese Unexamined Patent Publication No. 10-295366

化学と生物, Vol. 49, No. 4, pp. 256-260, 2011Chemistry and Biology, Vol. 49, No. 4, pp. 256-260, 2011

以上の通り、微生物を利用して塩素化エチレン等の揮発性有機塩素化合物を分解する方法は数多く報告されているが、未だ改善の余地が残されている。 As described above, many methods for decomposing volatile organic chlorine compounds such as chlorinated ethylene using microorganisms have been reported, but there is still room for improvement.

従って、本発明は、揮発性有機塩素化合物を浄化(分解)する新たな方法を提供することを目的とする。 Therefore, an object of the present invention is to provide a new method for purifying (decomposing) a volatile organic chlorine compound.

本発明者らが鋭意検討した結果、カタラーゼ生成能と、酸素の存在下で揮発性有機塩素化合物を分解する能力を有する細菌、及び過酸化水素を使用することによって、前記細菌が、カタラーゼの作用によって過酸化水素から供給される酸素を利用して、揮発性有機塩素化合物を効率的に分解できることを見出した。 As a result of diligent studies by the present inventors, by using a bacterium having a catalase-producing ability and an ability to decompose a volatile organochlorine compound in the presence of oxygen, and hydrogen peroxide, the bacterium acts as a catalase. It was found that volatile organochlorine compounds can be efficiently decomposed by using oxygen supplied from hydrogen peroxide.

即ち、本発明は以下を含む。
[1]カタラーゼ生成能と、酸素の存在下で揮発性有機塩素化合物を分解する能力とを有する細菌を過酸化水素の存在下で揮発性有機塩素化合物に作用させて、当該揮発性有機塩素化合物を分解する分解工程を含む、揮発性有機塩素化合物の浄化方法。
[2]前記揮発性有機塩素化合物がトリクロロエチレン及び/又はシス-1,2-ジクロロエチレンである、[1]に記載の方法。
[3]前記細菌がロドコッカス(Rhodococcus)属の細菌である、[1]又は[2]に記載の方法。
[4]前記ロドコッカス(Rhodococcus)属の細菌がロドコッカス・ジョスティ(Rhodococcus jostii)RHA1株である、[3]に記載の方法。
[5]前記揮発性有機塩素化合物が地下水に含まれており、当該地下水を原位置で浄化する、[1]〜[4]のいずれかに記載の方法。
[6]前記過酸化水素が、前記地下水に導入された後3日以内に消失して酸素に変換される、[5]に記載の方法。
[7]前記過酸化水素を、前記地下水中の濃度が0.02%以下になるように導入し、ロドコッカス・ジョスティ(Rhodococcus jostii)RHA1株を、前記地下水中の菌数が5.0×108cells/ml以上になるように導入する、[5]又は[6]に記載の方法。
That is, the present invention includes the following.
[1] A bacterium having a ability to generate catalase and an ability to decompose a volatile organochlorine compound in the presence of oxygen is allowed to act on the volatile organochlorine compound in the presence of hydrogen peroxide to cause the volatile organochlorine compound. A method for purifying volatile organochlorine compounds, which comprises a decomposition step of decomposing hydrogen peroxide.
[2] The method according to [1], wherein the volatile organochlorine compound is trichlorethylene and / or cis-1,2-dichloroethylene.
[3] The method according to [1] or [2], wherein the bacterium is a bacterium belonging to the genus Rhodococcus.
[4] The method according to [3], wherein the bacterium belonging to the genus Rhodococcus is a Rhodococcus jostii RHA1 strain.
[5] The method according to any one of [1] to [4], wherein the volatile organic chlorine compound is contained in the groundwater and the groundwater is purified in the original position.
[6] The method according to [5], wherein the hydrogen peroxide disappears and is converted into oxygen within 3 days after being introduced into the groundwater.
[7] The hydrogen peroxide was introduced so that the concentration in the groundwater was 0.02% or less, and the Rhodococcus jostii RHA1 strain was introduced into the groundwater with a bacterial count of 5.0 × 10 8 cells / ml. The method according to [5] or [6], which is introduced so as described above.

本発明によれば、所定の能力を有する細菌及び過酸化水素を使用するだけで、揮発性有機塩素化合物を効率的に分解することができる。 According to the present invention, a volatile organochlorine compound can be efficiently decomposed only by using a bacterium having a predetermined ability and hydrogen peroxide.

酸素を利用した揮発性有機塩素化合物の分解経路を示す。The decomposition route of volatile organic chlorine compounds using oxygen is shown. 様々な濃度の過酸化水素の存在下におけるRHA1株の生育曲線を示す。The growth curves of the RHA1 strain in the presence of hydrogen peroxide of various concentrations are shown. 様々な濃度の過酸化水素の存在下におけるRHA1株によるトリクロロエチレンの分解状況を示す。The decomposition status of trichlorethylene by the RHA1 strain in the presence of hydrogen peroxide of various concentrations is shown. 様々な濃度の過酸化水素の存在下における様々な濃度のTDR12株(揮発性有機塩素化合物の分解遺伝子を消失させたRHA1株の変異株)によるトリクロロエチレンの分解状況を示す。The decomposition status of trichlorethylene by the TDR12 strain (mutant strain of the RHA1 strain in which the degrading gene of the volatile organochlorine compound is eliminated) in the presence of various concentrations of hydrogen peroxide is shown. 様々な条件(対照、カタラーゼ試薬、又はRHA1株)における過酸化水素濃度の経時変化を示す。It shows the time course of hydrogen peroxide concentration under various conditions (control, catalase reagent, or RHA1 strain). 様々の濃度の過酸化水素の存在下における様々な濃度のRHA1株によるシス-1,2-ジクロロエチレンの分解試験における過酸化水素濃度の経時変化を示す。The time course of the hydrogen peroxide concentration in the decomposition test of cis-1,2-dichloroethylene by the RHA1 strain at various concentrations in the presence of hydrogen peroxide at various concentrations is shown. 様々の濃度の過酸化水素の存在下における様々な濃度のRHA1株によるシス-1,2-ジクロロエチレンの分解状況を示す。The decomposition status of cis-1,2-dichloroethylene by the RHA1 strain at various concentrations in the presence of hydrogen peroxide at various concentrations is shown. 過酸化水素の存在下における様々な濃度のRHA1株によるシス-1,2-ジクロロエチレンの分解試験における過酸化水素濃度の経時変化を示す。The time course of the hydrogen peroxide concentration in the decomposition test of cis-1,2-dichloroethylene by the RHA1 strain at various concentrations in the presence of hydrogen peroxide is shown. 過酸化水素の存在下における様々な濃度のRHA1株によるシス-1,2-ジクロロエチレンの分解状況を示す。The decomposition status of cis-1,2-dichloroethylene by the RHA1 strain at various concentrations in the presence of hydrogen peroxide is shown.

以下、本発明について詳細に説明する。 Hereinafter, the present invention will be described in detail.

本発明は、所定の能力を有する細菌を過酸化水素の存在下で揮発性有機塩素化合物に作用させて、当該揮発性有機塩素化合物を分解する分解工程を含む、揮発性有機塩素化合物の浄化方法に関する。 The present invention is a method for purifying a volatile organic chlorine compound, which comprises a decomposition step of allowing a bacterium having a predetermined ability to act on the volatile organic chlorine compound in the presence of hydrogen peroxide to decompose the volatile organic chlorine compound. Regarding.

所定の能力を有する細菌としては、カタラーゼ生成能と、酸素の存在下で揮発性有機塩素化合物を分解する能力を有するものを使用する。好ましくは、過酸化水素に対する耐性を更に有する細菌を使用する。 As the bacterium having a predetermined ability, a bacterium having a catalase-producing ability and an ability to decompose a volatile organic chlorine compound in the presence of oxygen is used. Preferably, a bacterium that is more resistant to hydrogen peroxide is used.

「カタラーゼ」とは、過酸化水素を酸素及び水に分解する酵素である。 "Catalase" is an enzyme that breaks down hydrogen peroxide into oxygen and water.

「過酸化水素に対する耐性」を有する細菌とは、過酸化水素の存在下においてもカタラーゼを生成して過酸化水素を酸素に変換できる細菌を意味する。具体的には、0.01%の濃度の過酸化水素の存在下、好ましくは0.05%の濃度の過酸化水素の存在下、より好ましくは0.1%の濃度の過酸化水素の存在下、更に好ましくは0.5%の濃度の過酸化水素の存在下においてもカタラーゼを生成して過酸化水素を酸素に変換できる細菌を意味する。 A bacterium having "resistance to hydrogen peroxide" means a bacterium capable of producing catalase and converting hydrogen peroxide into oxygen even in the presence of hydrogen peroxide. Specifically, in the presence of 0.01% hydrogen peroxide, preferably in the presence of 0.05% hydrogen peroxide, more preferably in the presence of 0.1% hydrogen peroxide, even more preferably 0.5. It means a bacterium that can generate catalase and convert hydrogen peroxide into oxygen even in the presence of hydrogen peroxide at a concentration of%.

揮発性有機塩素化合物の分解に使用される酸素は、空気中に含まれる酸素であってもよいし、カタラーゼの作用によって過酸化水素から生成される酸素であってもよい。 The oxygen used for decomposing the volatile organochlorine compound may be oxygen contained in the air or oxygen generated from hydrogen peroxide by the action of catalase.

本発明に係る方法では、前記細菌が酸素を利用して揮発性有機塩素化合物を効率的に分解することができる(図1)。 In the method according to the present invention, the bacterium can efficiently decompose volatile organic chlorine compounds using oxygen (Fig. 1).

カタラーゼ生成能と、酸素の存在下で揮発性有機塩素化合物を分解する能力を有する細菌として、ロドコッカス(Rhodococcus)属の細菌を使用することができる。ロドコッカス(Rhodococcus)属の細菌としては、ロドコッカス・アイシェンシス(Rhodococcus aichiensis)、ロドコッカス・オーランティアカス(Rhodococcus aurantiacus)、ロドコッカス・バイコヌレンシス(Rhodococcus baikonurensis)、ロドコッカス・ブロンキアリス(Rhodococcus bronchialis)、ロドコッカス・クロロフェノリカス(Rhodococcus chlorophenolicus)、ロドコッカス・チュブエンシス(Rhodococcus chubuensis)、ロドコッカス・コプロフィラス(Rhodococcus coprophilus)、ロドコッカス・コラリヌス(Rhodococcus corallinus)、ロドコッカス・コリネバクテリオイデス(Rhodococcus corynebacterioides)、ロドコッカス・エクイ(Rhodococcus equi)、ロドコッカス・エリスロポリス(Rhodococcus erythropolis)、ロドコッカス・ファシアンス(Rhodococcus fascians)、ロドコッカス・グロベルルス(Rhodococcus globerulus)、ロドコッカス・ジョスティ(Rhodococcus jostii)、ロドコッカス・コーリエンシス(Rhodococcus koreensis)、ロドコッカス・クロッペンステッティイ(Rhodococcus kroppenstedtii)、ロドコッカス・マンシャネシス(Rhodococcus maanshanensis)、ロドコッカス・マリノナセンス(Rhodococcus marinonascens)、ロドコッカス・マリス(Rhodococcus maris)、ロドコッカス・オパカス(Rhodococcus opacus)、ロドコッカス・ペルコラタス(Rhodococcus percolatus)、ロドコッカス・ピリジノボランス(Rhodococcus pyridinivorans)、ロドコッカス・ロドニ(Rhodococcus rhodnii)、ロドコッカス・ロドクロウス(Rhodococcus rhodochrous)、ロドコッカス・ルーバー(Rhodococcus ruber)、ロドコッカス・テラエ(Rhodococcus terrae)、ロドコッカス・トリアロマエ(Rhodococcus triatomae)、ロドコッカス・ツキサムエンシス(Rhodococcus tukisamuensis)、ロドコッカス・ラチスラヴィエンシス(Rhodococcus wratislaviensis)、ロドコッカス・ユンナネンシス(Rhodococcus yunnanensis)、ロドコッカス・ゾフィ(Rhodococcus zopfii)等を挙げることができる。 Bacteria of the genus Rhodococcus can be used as bacteria capable of producing catalase and decomposing volatile organochlorine compounds in the presence of oxygen. Bacteria of the genus Rhodococcus include Rhodococcus aichiensis, Rhodococcus aurantiacus, Rhodococcus baikonurensis, Rhodococcus baikonurensis, Rhodococcus bikonurensis, Rhodococcus bikonurensis, Rhodococcus bikonurensis, Rhodococcus bikonurensis (Rhodococcus chlorophenolicus), Rhodococcus chubuensis, Rhodococcus coprophilus, Rhodococcus corallinus, Rhodococcus corallinus, Rhodococcus corallinus, Rhodococcus corallinus, Rhodococcus corallinus, Rhodococcus corallinus, Rhodococcus corallinus Police (Rhodococcus erythropolis), Rhodococcus fascians, Rhodococcus globerulus, Rhodococcus jostii, Rhodococcus jostii, Rhodococcus koriences, Rhodococcus koredococcus Rhodococcus maanshanensis, Rhodococcus marinonascens, Rhodococcus maris, Rhodococcus opacus, Rhodococcus opacus, Rhodococcus rhodococcus (Rhodococcus rhodnii), Rhodococcus rhodochrous, Rhodococcus ruber, Rhodoc Rhodococcus terrae, Rhodococcus triatomae, Rhodococcus tukisamuensis, Rhodococcus wratislaviensis, Rhodococcus wratislaviensis, Rhodococcus wratislaviensis, Rhodococcus wratislaviensis ) Etc. can be mentioned.

特に限定するものではないが、揮発性有機塩素化合物をより効率的に分解するためには、ロドコッカス(Rhodococcus)属の細菌として、ロドコッカス・ジョスティ(Rhodococcus jostii)を使用することが好ましく、ロドコッカス・ジョスティ(Rhodococcus jostii)RHA1株(以下、単に「RHA1株」という)を使用することが特に好ましい。RHA1株は、製品評価技術基盤機構から入手することができる(NBRC 108803)。 Although not particularly limited, in order to decompose volatile organochlorine compounds more efficiently, it is preferable to use Rhodococcus jostii as a bacterium of the genus Rhodococcus, and Rhodococcus jostii is preferable. (Rhodococcus jostii) It is particularly preferable to use an RHA1 strain (hereinafter, simply referred to as "RHA1 strain"). The RHA1 strain can be obtained from the Product Evaluation Technology Infrastructure Organization (NBRC 108803).

RHA1株は、γ-ヘキサクロロシクロヘキサン汚染圃場から単離された好気性細菌であり、ポリ塩化ビフェニル(PCB)を分解するために広く使用されている(例えば、特許第2990016号)。RHA1株はPCBをビフェニル分解酵素系で共代謝する。ビフェニルはビフェニルジオキシゲナーゼ(BphA)、ジヒドロジオールデヒドロゲナーゼ(BphB)、2,3-ジヒドロキシビフェニル 1,2-ジオキシゲナーゼ(BphC)、及び2-ヒドロキシ-6-オキソ-6-フェニルヘキサ-2,4-ジエノエートヒドロラーゼ(BphD)からなる一連の反応により、安息香酸及び2-ヒドロキシペンタ-2,4-ジエン酸に変換される。BphDの反応で生じた2-ヒドロキシペンタ-2,4-ジエン酸はピルビン酸及びアセチル-CoAに変換され、安息香酸はカテコール及び3-オキシアジピン酸を経由してスクシニル-CoA及びアセチル-CoAに変換され、これらは最終的にクエン酸回路へ導かれ、炭素源及びエネルギー源として利用される。 The RHA1 strain is an aerobic bacterium isolated from a field contaminated with γ-hexachlorocyclohexane and is widely used for degrading polychlorinated biphenyls (PCBs) (eg, Patent No. 2990016). The RHA1 strain co-metabolizes PCBs with a biphenyl-degrading enzyme system. Biphenyls are biphenyldioxygenase (BphA), dihydrodiol dehydrogenase (BphB), 2,3-dihydroxybiphenyl 1,2-dioxygenase (BphC), and 2-hydroxy-6-oxo-6-phenylhexa-2,4- It is converted to benzoic acid and 2-hydroxypenta-2,4-dienoic acid by a series of reactions consisting of dienoate hydrolase (BphD). 2-Hydroxypenta-2,4-dienoic acid produced in the reaction of BphD is converted to pyruvic acid and acetyl-CoA, and benzoic acid is converted to succinyl-CoA and acetyl-CoA via catechol and 3-oxyadipic acid. Once converted, they are eventually led to the citric acid cycle for use as a carbon and energy source.

BphA、BphB、BphC、及びBphDのそれぞれについて、複数のアイソザイムの存在が明らかになっている。BphAにおいては、bphAaAb、etbAa1Ab1及びetbAa2Ab2にコードされる3種類のジオキシゲナーゼ成分で構成されるアイソザイムが見出されている。BphBにおいては、bphB1及びbphB2にコードされる2種類のアイソザイムが見出されている。BphCにおいては、bphC1及びetbCにコードされる2種類のアイソザイムが見出されている。BphDにおいては、bphD、etbD1、及びetbD2にコードされる3種類のアイソザイムが見出されている。これらの酵素遺伝子は、5つの酵素クラスターを形成して、巨大線状プラスミドpRHL1又はpRHL2上に分布している。 The existence of multiple isozymes has been clarified for each of BphA, BphB, BphC, and BphD. In BphA, an isozyme composed of three types of dioxygenase components encoded by bphAaAb, etbAa1Ab1 and etbAa2Ab2 has been found. In BphB, two isozymes encoded by bphB1 and bphB2 have been found. In BphC, two isozymes encoded by bphC1 and etbC have been found. In BphD, three isozymes encoded by bphD, etbD1 and etbD2 have been found. These enzyme genes form five enzyme clusters and are distributed on the giant linear plasmid pRHL1 or pRHL2.

RHA1株は、ビフェニルジオキシゲナーゼ(BphA及びEtbA)の水酸化反応によって揮発性有機塩素化合物を分解することができる。 The RHA1 strain can decompose volatile organochlorine compounds by the hydroxylation reaction of biphenyldioxygenases (BphA and EtbA).

揮発性有機塩素化合物としては、テトラクロロエチレン、トリクロロエチレン、シス-1,2-ジクロロエチレン、トランス-1,2-ジクロロエチレン、1,1-ジクロロエチレン、塩化ビニルモノマー等の塩素化エチレン類を挙げることができる。特に限定するものではないが、本発明に係る方法では、特にトリクロロエチレン及びシス-1,2-ジクロロエチレンを対象とする。 Examples of the volatile organochlorine compound include chlorinated ethylenes such as tetrachlorethylene, trichlorethylene, cis-1,2-dichloroethylene, trans-1,2-dichloroethylene, 1,1-dichloroethylene and vinyl chloride monomer. Although not particularly limited, the method according to the present invention particularly targets trichlorethylene and cis-1,2-dichloroethylene.

RHA1株を用いて塩素化エチレン(特にトリクロロエチレン及びシス-1,2-ジクロロエチレン)を分解する場合、分解過程において塩化ビニルモノマーが生成しないため、二次的な環境汚染を回避することができる。また、RHA1株は、浄化対象物質自体を誘導基質として利用できるため、トルエン、フェノール等の有害な誘導基質を使用する必要がなく、更なる環境汚染を回避することができる。更に、RHA1株は、誘導基質としてメタン等の水に溶解しにくい物質を使用する必要がないため、RHA1株と過酸化水素のみを浄化対象とする環境に導入することにより浄化を行うことができる。 When chlorinated ethylene (particularly trichlorethylene and cis-1,2-dichloroethylene) is decomposed using the RHA1 strain, vinyl chloride monomer is not produced in the decomposition process, so that secondary environmental pollution can be avoided. In addition, since the RHA1 strain can use the substance to be purified itself as an inducing substrate, it is not necessary to use harmful inducing substrates such as toluene and phenol, and further environmental pollution can be avoided. Furthermore, since the RHA1 strain does not need to use a substance that is difficult to dissolve in water such as methane as an inducing substrate, it can be purified by introducing only the RHA1 strain and hydrogen peroxide into an environment to be purified. ..

本発明に係る方法では、前記細菌が酸素を利用して揮発性有機塩素化合物を分解する。そのため、本発明に係る方法は好気環境で行うことができる。「好気環境」とは、前記細菌が揮発性有機塩素化合物を分解するのに十分な量の酸素が存在する環境である。好気環境としては、酸素が十分に存在する地上環境を挙げることができる。 In the method according to the present invention, the bacterium decomposes volatile organic chlorine compounds using oxygen. Therefore, the method according to the present invention can be performed in an aerobic environment. The "aerobic environment" is an environment in which a sufficient amount of oxygen is present for the bacteria to decompose volatile organochlorine compounds. Examples of the aerobic environment include a ground environment in which oxygen is sufficiently present.

本発明に係る方法では、前記細菌が有するカタラーゼの作用により過酸化水素から酸素を供給することができる。そのため、本発明に係る方法は酸素が少ない微好気環境や酸素が無い嫌気環境で行うこともできる。「微好気環境」とは、酸素が存在するが、前記細菌が揮発性有機塩素化合物を分解するのに十分な量の酸素は存在しない環境である。「嫌気環境」とは、酸素が全く存在しない環境である。微好気環境又は嫌気環境としては、酸素が十分に存在しない又は全く存在しない地下環境、例えば、地下水、地下土壌等を挙げることができる。 In the method according to the present invention, oxygen can be supplied from hydrogen peroxide by the action of catalase possessed by the bacterium. Therefore, the method according to the present invention can also be performed in a microaerobic environment with little oxygen or an anaerobic environment without oxygen. The "microaerobic environment" is an environment in which oxygen is present but not in a sufficient amount for the bacteria to decompose volatile organochlorine compounds. An "anaerobic environment" is an environment in which oxygen is completely absent. Examples of the microaerobic environment or the anaerobic environment include underground environments in which oxygen is not sufficiently present or not present at all, such as groundwater and underground soil.

例えば、本発明の一実施形態では、前記細菌及び過酸化水素を揮発性有機塩素化合物で汚染された地下環境に注入して、当該地下環境を浄化する方法を対象とする。本発明の更なる実施形態では、前記細菌及び過酸化水素を揮発性有機塩素化合物を含む地下水に注入して、当該地下水を原位置で浄化する方法を対象とする。 For example, in one embodiment of the present invention, a method of injecting the bacteria and hydrogen peroxide into an underground environment contaminated with a volatile organochlorine compound to purify the underground environment is targeted. A further embodiment of the present invention covers a method of injecting the bacteria and hydrogen peroxide into groundwater containing a volatile organochlorine compound to purify the groundwater in situ.

従来、好気性細菌を利用して地下環境の汚染を浄化する場合、地下環境に酸素を導入する必要があった。地下環境に酸素を導入する方法としては、過酸化マグネシウムを主成分とする酸素徐放剤の注入、高濃度酸素水の注入、マイクロナノレベル微細酸素気泡の注入、オゾンの注入、エアスパージング等が知られている。一方、本発明に係る方法では、カタラーゼ生成能を有する細菌及び過酸化水素を注入することによって、カタラーゼの作用により過酸化水素から酸素を供給することができる。過酸化水素を利用することにより、地下環境への酸素供給効率を上げることができ、且つ地下環境への酸素供給コストを下げることができる。 Conventionally, when purifying pollution in the underground environment using aerobic bacteria, it has been necessary to introduce oxygen into the underground environment. Methods for introducing oxygen into the underground environment include injection of an oxygen sustained-release agent containing magnesium peroxide as the main component, injection of high-concentration oxygen water, injection of micro-nano-level fine oxygen bubbles, ozone injection, air sparging, etc. Are known. On the other hand, in the method according to the present invention, oxygen can be supplied from hydrogen peroxide by the action of catalase by injecting a bacterium capable of producing catalase and hydrogen peroxide. By using hydrogen peroxide, the efficiency of oxygen supply to the underground environment can be increased, and the cost of supplying oxygen to the underground environment can be reduced.

一方、地下環境に過酸化水素を注入することによって、過酸化水素は細菌が生成するカタラーゼによって酸素を生成するだけでなく、過酸化水素が地盤中の鉄化合物等の触媒物質と反応(ヒドロキシラジカル反応)することによっても酸素が生成する。ヒドロキシラジカル反応が起こると細菌に有害なヒドロキシラジカルが発生して細菌が死滅する。本発明者らは、細菌によるカタラーゼ反応が地盤中のヒドロキシラジカル反応より速く進行することを発見したため、過酸化水素をできるだけカタラーゼ反応によって酸素に変換するため、一定濃度の細菌を過酸化水素と共に地盤に導入することの重要性が明らかとなった。 On the other hand, by injecting hydrogen peroxide into the underground environment, hydrogen peroxide not only produces oxygen by catalase generated by bacteria, but also hydrogen peroxide reacts with catalytic substances such as iron compounds in the ground (hydroxy radicals). Oxygen is also generated by the reaction). When a hydroxyl radical reaction occurs, hydroxyl radicals that are harmful to the bacterium are generated and the bacterium is killed. Since the present inventors have discovered that the catalase reaction by bacteria proceeds faster than the hydroxyl radical reaction in the ground, in order to convert hydrogen peroxide into oxygen by the catalase reaction as much as possible, a certain concentration of bacteria is mixed with hydrogen peroxide in the ground. The importance of introducing it to the above became clear.

過酸化水素は、前記細菌が揮発性有機塩素化合物を分解するのに十分な酸素が供給され、且つヒドロキシラジカルの生成がなるべく抑えられる濃度となるように、地下環境に注入されることが好ましい。具体的な過酸化水素濃度は、使用する細菌の種類、地下環境に残存する酸素の濃度等に応じて適宜変更されるが、過酸化水素濃度が0.02%であれば酸素は十分に供給され、その際RHA1株が地下水中に5×108cells/mLの濃度で存在すれば、RHA1株のヒドロキシラジカルによる阻害を小さくできる。そのため、地下水中の過酸化水素濃度が0.02%以下となり、且つRHA1株が地下水中に5×108cells/mL以上の濃度になるように注入量を調整することが好ましい。地下水中の過酸化水素濃度の下限は、例えば、0.01%、0.005%、0.001%等としてもよい。地下水中のRHA1株濃度の上限は、例えば、1×109cells/mL、5×109cells/mL、1×1010cells/mL等としてもよい。 Hydrogen peroxide is preferably injected into the underground environment so that sufficient oxygen is supplied to the bacteria to decompose the volatile organic chlorine compounds and the concentration of hydroxyl radicals is suppressed as much as possible. The specific hydrogen peroxide concentration is appropriately changed according to the type of bacteria used, the concentration of oxygen remaining in the groundwater, etc. However, if the hydrogen peroxide concentration is 0.02%, oxygen is sufficiently supplied. if present at a concentration of that time RHA1 strain groundwater 5 × 10 8 cells / mL, can be reduced inhibition by hydroxy radicals RHA1 strain. Therefore, the hydrogen peroxide concentration in groundwater is 0.02% or less, and RHA1 strain it is preferable to adjust the injection amount to a concentration of more than 5 × 10 8 cells / mL in groundwater. The lower limit of the hydrogen peroxide concentration in the groundwater may be, for example, 0.01%, 0.005%, 0.001% or the like. The upper limit of the RHA1 strain concentration in groundwater may be, for example, 1 × 10 9 cells / mL, 5 × 10 9 cells / mL, 1 × 10 10 cells / mL, or the like.

以下、実施例を用いて本発明をより詳細に説明するが、本発明の技術的範囲はこれに限定されるものではない。 Hereinafter, the present invention will be described in more detail with reference to examples, but the technical scope of the present invention is not limited thereto.

[実施例1]RHA1株の過酸化水素に対する耐性評価試験
本試験では、RHA1株の過酸化水素に対する耐性を評価するために、過酸化水素濃度を段階的に変化させたコハク酸培地においてRHA1株の増殖状況を確認した。
[Example 1] Resistance evaluation test of RHA1 strain to hydrogen peroxide In this test, in order to evaluate the resistance of RHA1 strain to hydrogen peroxide, the RHA1 strain was placed in a succinic acid medium in which the hydrogen peroxide concentration was gradually changed. The growth status of hydrogen peroxide was confirmed.

10mlのLB液体培地(1 g/l Bacto tryptone、0.5 g/l Yeast extract、0.5 g/l NaCl)にRHA1株を植菌して、一昼夜培養した。培養液から菌体を遠心分離(5,000 rpm、5分、4℃)によって回収し、5 mlのW無機塩培地(表1)で2回洗浄後、1 mlのW無機塩培地に菌体を懸濁した。5 ml容量の小型L字管中に、培養液をOD600が0.4になるようにW無機塩培地で5 ml調製した。培地には炭素源として終濃度10 mMのコハク酸を添加し、過酸化水素を終濃度が0%、0.01%、0.05%、0.1%、0.5%、1.0%になるように添加した。小型L字管を自動OD測定培養機(ADVANTEC)に設置し、70 rpmの回転数及び30℃で培養した。培養液の懸度(660 nmでの吸光度)を1時間置きに自動的に測定して記録した。 The RHA1 strain was inoculated into 10 ml of LB liquid medium (1 g / l Bacto tryptone, 0.5 g / l Yeast extract, 0.5 g / l NaCl) and cultured overnight. The cells were collected from the culture medium by centrifugation (5,000 rpm, 5 minutes, 4 ° C), washed twice with 5 ml of W inorganic salt medium (Table 1), and then the cells were placed in 1 ml of W inorganic salt medium. Suspended. In a small L-shaped tube having a capacity of 5 ml, 5 ml of the culture solution was prepared with W inorganic salt medium so that the OD600 was 0.4. Succinic acid having a final concentration of 10 mM was added to the medium as a carbon source, and hydrogen peroxide was added so that the final concentrations were 0%, 0.01%, 0.05%, 0.1%, 0.5%, and 1.0%. A small L-shaped tube was placed in an automatic OD measurement incubator (ADVANTEC) and cultured at a rotation speed of 70 rpm and 30 ° C. The culture broth (absorbance at 660 nm) was automatically measured and recorded every hour.

試験の結果を図2に示す。過酸化水素濃度0%では、培養6時間から30時間にかけて対数増殖期が観察され、40時間でA660が1.3程度となって定常期に達した。これと同様の生育が、過酸化水素濃度0.01%及び0.05%でも観察された。過酸化水素濃度0.1%では、生育の誘導期が約3倍に延びて生育の遅延が観察されたが、対数増殖期の増殖速度は過酸化水素濃度0%の場合とほぼ同様であった。過酸化水素濃度0.5%では、生育能の低下が観察されたが、培養70時間でA660が0.6程度になるまで増殖した。過酸化水素濃度1.0%では、培養6時間でA660が低下し、そのまま増殖しなかった。 The results of the test are shown in FIG. At a hydrogen peroxide concentration of 0%, a logarithmic growth phase was observed from 6 hours to 30 hours of culturing, and A660 reached about 1.3 in 40 hours, reaching a steady phase. Similar growth was observed at hydrogen peroxide concentrations of 0.01% and 0.05%. At a hydrogen peroxide concentration of 0.1%, the growth induction period was extended about three times and growth was delayed, but the growth rate during the logarithmic growth period was almost the same as when the hydrogen peroxide concentration was 0%. At a hydrogen peroxide concentration of 0.5%, a decrease in viability was observed, but the cells grew until A660 reached about 0.6 after 70 hours of culturing. At a hydrogen peroxide concentration of 1.0%, A660 decreased after 6 hours of culturing and did not grow as it was.

以上の結果から、RHA1株は少なくとも0.5%までの過酸化水素に対して耐性を有することが示唆された。一方、大腸菌では0.6 mM(≒0.002%)の過酸化水素に対しても感受性を示すことが報告されている。そのため、RHA1株の過酸化水素に対する耐性は高いと判断される。 These results suggest that the RHA1 strain is resistant to hydrogen peroxide up to at least 0.5%. On the other hand, it has been reported that Escherichia coli is sensitive to hydrogen peroxide of 0.6 mM (≈0.002%). Therefore, it is judged that the resistance of the RHA1 strain to hydrogen peroxide is high.

Figure 0006913454
Figure 0006913454

[実施例2]RHA1株のトリクロロエチレン(TCE)分解能に対する過酸化水素の影響評価試験
本試験では、RHA1株のトリクロロエチレン分解能に対する過酸化水素の影響を評価するために、過酸化水素濃度を段階的に変化させたコハク酸培地においてトリクロロエチレンの分解試験を行った。
[Example 2] Evaluation test of the effect of hydrogen peroxide on the trichlorethylene (TCE) resolution of the RHA1 strain In this test, in order to evaluate the effect of hydrogen peroxide on the trichlorethylene (TCE) resolution of the RHA1 strain, the hydrogen peroxide concentration was stepwise. A degradation test of trichlorethylene was carried out in a modified succinic acid medium.

20 mMのコハク酸を含むW無機塩培地を200 ml用意し、そこにLB培地で一昼夜培養したRHA1株をOD600が0.1になるように加え、120 rpm及び30℃で24時間培養した。その後、培養液に4 mmol(20 mM分)のコハク酸を追加し、更に24時間培養した。培養後の菌体を遠心分離(5,000 rpm、5分、4℃)により回収し、30 mlのW無機塩培地を用いて菌体洗浄を2回繰り返した。100 mlの褐色ガラスバイアル中に、W無機塩培地を用いて、OD600が10(≒1.0×108cfu/ml)の懸濁液を20 ml調製した。懸濁液に終濃度が10 mg/lとなるようにトリクロロエチレンを加え、速やかにテフロンコートされたブチルゴム栓で密栓し、トリクロロエチレンの気液平衡の安定化のために180 rpm及び30℃で1時間振盪した。試験期間中、バイアルをインキュベーターで保管し、180 rpm及び30℃で振盪し続けた。過酸化水素は0日目の測定直後にマイクロシリンジで終濃度が0%、0.01%、0.05%、0.1%、0.5%となるように、ゴム栓からバイアルに直接注射して添加した。トリクロロエチレンの定量は、バイアルの上部からガスタイトシリンジを用いて400 μlの気相サンプルを採取してガスクロマトグラフィー−水素炎イオン化検出器(GC-FID)で分析した。解析では、トリクロロエチレンに由来するピークから面積を算出し、測定開始時のピーク面積を基準として、バイアル内に残存するトリクロロエチレンの割合を日数経過ごとに求めた。 200 ml of W inorganic salt medium containing 20 mM succinic acid was prepared, and RHA1 strain cultured in LB medium for 24 hours was added so that OD600 was 0.1, and cultured at 120 rpm and 30 ° C. for 24 hours. Then, 4 mmol (20 mM) of succinic acid was added to the culture broth, and the cells were further cultured for 24 hours. After culturing, the cells were collected by centrifugation (5,000 rpm, 5 minutes, 4 ° C.), and the cells were washed twice using 30 ml of W inorganic salt medium. In a 100 ml brown glass vial, 20 ml of a suspension having an OD600 of 10 (≈1.0 × 10 8 cfu / ml) was prepared using W inorganic salt medium. Trichlorethylene was added to the suspension to a final concentration of 10 mg / l, immediately sealed with a Teflon-coated butyl rubber stopper, and at 180 rpm and 30 ° C for 1 hour to stabilize the vapor-liquid equilibrium of trichlorethylene. It was shaken. During the test period, the vials were stored in an incubator and continued to shake at 180 rpm and 30 ° C. Immediately after the measurement on the 0th day, hydrogen peroxide was added by injecting directly into the vial from a rubber stopper so that the final concentration was 0%, 0.01%, 0.05%, 0.1%, 0.5% with a microsyringe. Trichloroethylene was quantified by taking a 400 μl gas phase sample from the top of the vial using a gas tight syringe and analyzing it with a gas chromatography-flame ionization detector (GC-FID). In the analysis, the area was calculated from the peak derived from trichlorethylene, and the proportion of trichlorethylene remaining in the vial was determined for each number of days based on the peak area at the start of measurement.

試験の結果を図3に示す。RHA1株は、過酸化水素濃度0.1%までは、過酸化水素が存在しない条件と同様にトリクロロエチレンを分解した。過酸化水素濃度0.5%ではトリクロロエチレン分解能の低下が若干見られたが、3日間でトリクロロエチレンを95%程度まで分解した。 The results of the test are shown in FIG. The RHA1 strain decomposed trichlorethylene up to a hydrogen peroxide concentration of 0.1% in the same manner as in the absence of hydrogen peroxide. Although a slight decrease in trichlorethylene resolution was observed at a hydrogen peroxide concentration of 0.5%, trichlorethylene was decomposed to about 95% in 3 days.

比較対照試験として、RHA1株由来のbphT1、bphT2二重遺伝子破壊株(TDR12株)を用いて、過酸化水素存在下におけるトリクロロエチレンの分解試験を行った。RHA1株のトリクロロエチレン分解を担うビフェニルジオキシゲナーゼBphA及びEtbAの発現は、2組のBphS-BphT二成分制御システムにより転写レベルでポジティブに制御されている。bphT1、bphT2二重遺伝子破壊によってトリクロロエチレン分解能を封じたRHA1株由来のTDR12株を本試験で使用した。 As a comparative control test, a trichlorethylene degradation test was conducted in the presence of hydrogen peroxide using a bphT1 and bphT2 double gene disruption strain (TDR12 strain) derived from the RHA1 strain. The expression of biphenyldioxygenases BphA and EtbA, which are responsible for the trichlorethylene degradation of the RHA1 strain, is positively regulated at the transcriptional level by two sets of BphS-BphT two-component control systems. The TDR12 strain derived from the RHA1 strain whose trichlorethylene resolution was blocked by the bphT1 and bphT2 double gene disruption was used in this study.

上記と同様の条件で試験を行った結果、過酸化水素濃度0.1%までは、トリクロロエチレンの分解は観察されなかった(図4)。過酸化水素濃度0.5%では約4割のトリクロロエチレンの分解が観察された。以上の結果から、TDR12株はトリクロロエチレンを分解しないことが示された。過酸化水素濃度0.5%におけるトリクロロエチレンの部分的な分解は、菌体を触媒とした過酸化水素によるトリクロロエチレンの化学的な分解(ヒドロキシラジカル反応)であると推察された。 As a result of conducting the test under the same conditions as above, no decomposition of trichlorethylene was observed up to a hydrogen peroxide concentration of 0.1% (Fig. 4). Decomposition of about 40% of trichlorethylene was observed at a hydrogen peroxide concentration of 0.5%. From the above results, it was shown that the TDR12 strain does not decompose trichlorethylene. The partial decomposition of trichlorethylene at a hydrogen peroxide concentration of 0.5% was presumed to be the chemical decomposition of trichlorethylene (hydroxy radical reaction) by hydrogen peroxide catalyzed by cells.

以上の結果から、過酸化水素を添加した培地(土壌のように触媒物質が存在しない環境)においては、過酸化水素濃度が0.1%以下であると、過酸化水素による阻害を受けずにRHA1株がトリクロロエチレンを分解することが示された。 From the above results, in a medium containing hydrogen peroxide (an environment in which no catalytic substance is present such as soil), if the hydrogen peroxide concentration is 0.1% or less, the RHA1 strain is not inhibited by hydrogen peroxide. Was shown to degrade trichlorethylene.

[実施例3]RHA1株のカタラーゼ生成能の確認試験
本試験では実汚染地下水中において、過酸化水素がRHA1株から生成されるカタラーゼによって分解されるかを確認するためにRHA1株と市販のカタラーゼ試薬を用いて試験を行った。
[Example 3] Confirmation test of catalase-producing ability of RHA1 strain In this test, RHA1 strain and commercially available catalase were used to confirm whether hydrogen peroxide was decomposed by catalase produced from RHA1 strain in actual contaminated groundwater. The test was performed using reagents.

100 mlのLB液体培地(1 g/l Bacto tryptone、0.5 g/l Yeast extract、0.5 g/l NaCl)にRHA1株を植菌して、一昼夜培養した。20 mMのコハク酸、1 g/lの酵母エキス、5 mMの硫酸アンモニウムを添加したW無機塩培地(SYW培地)を200 ml用意し、そこにLB液体培地で一昼夜培養したRHA1株を加え、100 rpm及び30℃で48時間培養した。培養後の菌体を遠心分離(5,000 rpm、10分、4℃)により回収し、W無機塩培地を用いて菌体洗浄を行ったものを分解試験に使用した。 The RHA1 strain was inoculated into 100 ml of LB liquid medium (1 g / l Bacto tryptone, 0.5 g / l Yeast extract, 0.5 g / l NaCl) and cultured overnight. Prepare 200 ml of W inorganic salt medium (SYW medium) supplemented with 20 mM succinic acid, 1 g / l yeast extract, and 5 mM ammonium sulfate, and add the RHA1 strain cultured overnight in LB liquid medium to 100. The cells were cultured at rpm and 30 ° C. for 48 hours. The cells after culturing were collected by centrifugation (5,000 rpm, 10 minutes, 4 ° C.), and the cells were washed with W inorganic salt medium and used for the decomposition test.

表2に試験条件を示す。条件2はウシ肝臓由来のカタラーゼ溶液を、条件3はRHA1株をそれぞれ添加した。カタラーゼはリン酸緩衝液に溶解して、0.02%過酸化水素が全て分解するのに必要な量のカタラーゼ溶液を添加した。条件1はRHA1株及びカタラーゼ試薬を添加しない対照区とした。それぞれ使用するバイアル瓶に地下水、菌液を投入後、過酸化水素、カタラーゼ試薬をバイアル瓶内に添加した。ブチルゴム栓とアルミシールにより密栓した後、手動により攪拌して均質化し、20 ℃の恒温槽内で静置培養を行った。各条件のバイアル瓶を複数本作成し,0、3、7日経過後にバイアル瓶を開栓して上澄み液をピペットで採取して分析を行った。 Table 2 shows the test conditions. Condition 2 was a catalase solution derived from bovine liver, and condition 3 was a RHA1 strain. Catalase was dissolved in phosphate buffer and the amount of catalase solution required for the complete decomposition of 0.02% hydrogen peroxide was added. Condition 1 was a control group to which the RHA1 strain and the catalase reagent were not added. After adding groundwater and bacterial solution to the vials to be used, hydrogen peroxide and catalase reagents were added to the vials. After sealing with a butyl rubber stopper and an aluminum seal, the mixture was manually stirred and homogenized, and then statically cultured in a constant temperature bath at 20 ° C. Multiple vials under each condition were prepared, and after 0, 3, and 7 days had passed, the vials were opened and the supernatant was collected with a pipette for analysis.

図5に各条件の過酸化水素濃度の経時変化を示す。RHA1株を添加した条件3及びカタラーゼ溶液を添加した条件2では、過酸化水素全量が試験開始直後に消費された。この結果よりRHA1株はカタラーゼを生成し、過酸化水素を分解したことが示された。一方でRHA1株、カタラーゼ溶液を添加しなかった条件1では過酸化水素が残存した。 FIG. 5 shows the change over time in the hydrogen peroxide concentration under each condition. Under condition 3 to which the RHA1 strain was added and condition 2 to which the catalase solution was added, the total amount of hydrogen peroxide was consumed immediately after the start of the test. From this result, it was shown that the RHA1 strain produced catalase and decomposed hydrogen peroxide. On the other hand, hydrogen peroxide remained under condition 1 in which the RHA1 strain and the catalase solution were not added.

以上の結果より、RHA1株はカタラーゼを生成し過酸化水素を瞬時に分解して酸素を生成していることが示された。 From the above results, it was shown that the RHA1 strain produced catalase and instantly decomposed hydrogen peroxide to produce oxygen.

Figure 0006913454
Figure 0006913454

[実施例4]実汚染地下水を用いたRHA1株と過酸化水素の同時導入によるシス-1,2-ジクロロエチレン分解試験
本試験では、実汚染サイトの地下水中においてRHA1株と過酸化水素を同時に導入して、過酸化水素の分解に伴う酸素供給によりシス-1,2-ジクロロエチレン(cis-DCE)が分解するか検討を行った。
[Example 4] Sis-1,2-dichloroethylene decomposition test by simultaneous introduction of RHA1 strain and hydrogen peroxide using actual contaminated groundwater In this test, RHA1 strain and hydrogen peroxide were introduced simultaneously in the groundwater of the actual contaminated site. Then, it was examined whether cis-1,2-dichloroethylene (cis-DCE) was decomposed by the oxygen supply accompanying the decomposition of hydrogen peroxide.

表3に試験条件を示す。それぞれ使用するバイアル瓶に少量の土壌(砂質土)、地下水、実施例3と同様の方法で調製した菌液を投入後、cis-DCE濃縮液及び過酸化水素をバイアル瓶内が満水となるように予め投入量を計算して添加した。ブチルゴム栓とアルミシールにより密栓した後、手動により土壌と地下水を攪拌して均質化し、20 ℃の恒温槽内で静置培養を行った。各条件のバイアル瓶を複数本作成し,0、1、3、7日経過後にバイアル瓶を開栓して上澄み液をピペットで採取して分析を行った。菌体量はRHA1株を未添加、1.0×108 cells/ml、5.0×108 cells/mlの3条件で評価した。また、添加する過酸化水素は液相部における終濃度で0.02%と0.1%の2条件を検討した。 Table 3 shows the test conditions. After adding a small amount of soil (sandy soil), groundwater, and the bacterial solution prepared in the same manner as in Example 3 into the vials to be used, the vial is filled with cis-DCE concentrate and hydrogen peroxide. As described above, the input amount was calculated in advance and added. After sealing with a butyl rubber stopper and an aluminum seal, the soil and groundwater were manually stirred and homogenized, and statically cultured in a constant temperature bath at 20 ° C. Multiple vials under each condition were prepared, and after 0, 1, 3, and 7 days had passed, the vials were opened and the supernatant was collected with a pipette for analysis. The amount of cells was evaluated under three conditions of 1.0 × 10 8 cells / ml and 5.0 × 10 8 cells / ml without adding RHA1 strain. In addition, the final concentration of hydrogen peroxide to be added in the liquid phase was 0.02% and 0.1%.

図6に各条件の過酸化水素濃度の経時変化を示す。この結果、試験開始直後に過酸化水素がカタラーゼ反応によって全て消費された条件(即ち、過酸化水素が残存することによりヒドロキシラジカル反応が生じてRHA1株が阻害されることのない条件)は条件1-2、条件1-3、条件1-6であることが確認できた。条件1-5は過酸化水素濃度に対してRHA1株の導入量が少なく、ヒドロキシラジカル反応によってRHA1株がダメージを受け、カタラーゼが生成しなくなったと考えられる。 FIG. 6 shows the change over time in the hydrogen peroxide concentration under each condition. As a result, the condition that hydrogen peroxide is completely consumed by the catalase reaction immediately after the start of the test (that is, the condition that the hydroxyl radical reaction does not occur due to the residual hydrogen peroxide and the RHA1 strain is not inhibited) is condition 1. It was confirmed that -2, condition 1-3, and condition 1-6. Under conditions 1-5, the amount of RHA1 strain introduced was small relative to the hydrogen peroxide concentration, and it is considered that the RHA1 strain was damaged by the hydroxyl radical reaction and catalase was no longer produced.

図7に試験開始直後に過酸化水素がカタラーゼ反応によって全て消費された条件におけるcis-DCE残存率を示す。条件1-2では試験開始直後に導入した過酸化水素は酸素に変換されたが、cis-DCEの分解はほとんどみられなかったため、導入したRHA1株菌体濃度が足りていないと考えられた。RHA1株菌体濃度が同様の条件である条件1-3及び条件1-6を比較すると、過酸化水素濃度が低い0.02%の方でcis-DCEが良く分解していることが示され、水中の過酸化水素濃度が0.02%であれば分解に必要な酸素が十分に確保できることが示された。 FIG. 7 shows the residual rate of cis-DCE under the condition that hydrogen peroxide was completely consumed by the catalase reaction immediately after the start of the test. Under condition 1-2, the hydrogen peroxide introduced immediately after the start of the test was converted to oxygen, but the decomposition of cis-DCE was hardly observed, so it was considered that the concentration of the introduced RHA1 strain cells was insufficient. Comparing conditions 1-3 and 1-6, which have similar RHA1 strain cell concentrations, it was shown that cis-DCE decomposed better at 0.02%, which has a lower hydrogen peroxide concentration, and in water. It was shown that if the hydrogen peroxide concentration is 0.02%, sufficient oxygen required for decomposition can be secured.

以上の結果より、過酸化水素全量をカタラーゼ反応によって短時間で酸素に変換する条件(即ち、導入したRHA1株がヒドロキシラジカル反応によって阻害を受けにくい条件)は、過酸化水素濃度を必要な酸素量を確保できる範囲内でできるだけ少なくすることが重要であり、本試験ではRHA1株の菌数が5×108cells/mLに対して、過酸化水素濃度を0.02%に設定することが最適であることが示された。 Based on the above results, the condition for converting the entire amount of hydrogen peroxide into oxygen in a short time by the catalase reaction (that is, the condition that the introduced RHA1 strain is not easily inhibited by the hydroxyl radical reaction) is that the hydrogen peroxide concentration is the required amount of oxygen. It is important to reduce the amount of radicals as much as possible within the range that can be secured, and in this test, it is optimal to set the hydrogen peroxide concentration to 0.02% for the number of RHA1 strains of 5 × 10 8 cells / mL. Was shown.

Figure 0006913454
Figure 0006913454

[実施例5]実汚染帯水層を模擬した環境におけるRHA1株と過酸化水素添加によるシス-1,2-ジクロロエチレン分解試験
本試験では、実汚染サイトの帯水層(土壌と地下水が存在する模擬環境)においてRHA1株と過酸化水素を添加して、cis-DCEが分解するか検討を行った。
[Example 5] Sis-1,2-dichloroethylene decomposition test by adding RHA1 strain and hydrogen peroxide in an environment simulating an actual contaminated aquifer In this test, an aquifer (soil and groundwater) at an actual contaminated site is present. In a simulated environment), RHA1 strain and hydrogen peroxide were added, and it was examined whether cis-DCE was decomposed.

表4に試験条件を示す。バイアル瓶に土壌、地下水(全ての条件で気相部がほとんど無くなるように設定)、実施例3と同様にRHA1株を培養及び洗浄した菌液を投入後、cis-DCE濃縮液及び過酸化水素を添加し、ブチルゴム栓で密栓した。この試験では実施例4の試験と比較して土壌の量を1 gから50 gに変更して実施した。密閉後のバイアル瓶は手動により土壌と地下水を攪拌して均質化した後、20℃の恒温槽内で静置培養を行った。各条件につきバイアル瓶を複数本作成し、0、3、7日経過後に開栓して静置した状態で上澄み液を採取して分析を行った。本試験では瓶の底部から約4割が土壌で浸漬する条件に対して終濃度で0.02%の過酸化水素を加え、RHA1株の導入量によるcis-DCEの分解量を評価した。 Table 4 shows the test conditions. Soil, groundwater (set so that the gas phase part is almost eliminated under all conditions), and the bacterial solution obtained by culturing and washing the RHA1 strain in the same manner as in Example 3 are added to the vial, and then the cis-DCE concentrate and hydrogen peroxide are added. Was added, and the mixture was sealed with a butyl rubber stopper. In this test, the amount of soil was changed from 1 g to 50 g as compared with the test of Example 4. The sealed vial was manually agitated and homogenized with soil and groundwater, and then statically cultured in a constant temperature bath at 20 ° C. Multiple vials were prepared for each condition, and after 0, 3, and 7 days, the supernatant was collected and analyzed in a state where the bottle was opened and allowed to stand. In this test, 0.02% hydrogen peroxide was added at a final concentration under the condition that about 40% of the bottle was immersed in soil, and the amount of cis-DCE decomposed by the amount of RHA1 strain introduced was evaluated.

図8に各条件の過酸化水素濃度の経時変化を示し,図9にcis-DCE残存率を示す。図8より各条件における開始直後の過酸化水素濃度が異なるのは、過酸化水素が添加した瞬時に土壌中の触媒物質との反応およびRHA1株が産生するカタラーゼとの反応により消費されたことで、初期濃度に差が見られた。実施例4の条件1-1と、過酸化水素を終濃度で0.02%添加してRHA1株を導入しない本試験の条件2-1とを比較すると、土壌を多く添加した条件2-1では3日間で過酸化水素が消失した。これは土壌量が多くなり触媒物質が増加したことによって、ヒドロキシラジカル反応による過酸化水素の消費が早くなったことが示された。条件2-2では過酸化水素が消失した3日目以降にcis-DCEが減少しなかったが、条件2-3ではRHA1株を導入しなかった条件2-1と比較しても明確にcis-DCEの減少が確認されたことからRHA1株による生分解が行われたことが推察された。なお、過酸化水素は3日以内に酸素に分解されたが、3日目以降のRHA1株による生分解はバイアル瓶内に残存していた酸素を消費することで進行したと思われる。 FIG. 8 shows the change over time in the hydrogen peroxide concentration under each condition, and FIG. 9 shows the residual rate of cis-DCE. From FIG. 8, the difference in the hydrogen peroxide concentration immediately after the start under each condition is that the hydrogen peroxide was consumed by the reaction with the catalyst substance in the soil and the reaction with the catalase produced by the RHA1 strain at the moment when the hydrogen peroxide was added. , There was a difference in the initial concentration. Comparing the condition 1-1 of Example 4 with the condition 2-1 of this test in which 0.02% of hydrogen peroxide was added at the final concentration and the RHA1 strain was not introduced, the condition 2-1 with a large amount of soil added was 3 Hydrogen peroxide disappeared in days. It was shown that the consumption of hydrogen peroxide by the hydroxyl radical reaction became faster due to the increase in the amount of soil and the increase in the catalyst substance. Under condition 2-2, cis-DCE did not decrease after the 3rd day when hydrogen peroxide disappeared, but under condition 2-3, it was clearly cis compared with condition 2-1 in which the RHA1 strain was not introduced. -Since a decrease in DCE was confirmed, it was inferred that biodegradation was performed by the RHA1 strain. Hydrogen peroxide was decomposed into oxygen within 3 days, but biodegradation by the RHA1 strain after the 3rd day seems to have proceeded by consuming the oxygen remaining in the vial.

以上の結果より、終濃度で0.02%の過酸化水素添加量に対して5×108cells/mL以上のRHA1株を帯水層に導入し、3日以内に地下水中の過酸化水素が完全に消失していれば、RHA1株の導入によってcis-DCEの浄化を行うことができることが示された。 Based on the above results, 5 × 10 8 cells / mL or more of RHA1 strain was introduced into the aquifer with respect to the final concentration of 0.02% hydrogen peroxide addition, and the hydrogen peroxide in the groundwater was completely eliminated within 3 days. It was shown that cis-DCE can be purified by introducing the RHA1 strain.

Figure 0006913454
Figure 0006913454

Claims (1)

カタラーゼ生成能と、酸素の存在下で揮発性有機塩素化合物を分解する能力とを有する細菌を過酸化水素の存在下で揮発性有機塩素化合物に作用させて、当該揮発性有機塩素化合物を分解する分解工程を含み、前記細菌がロドコッカス(Rhodococcus)属の細菌であるロドコッカス・ジョスティ(Rhodococcus jostii)RHA1株であり、
前記揮発性有機塩素化合物が地下水に含まれており、当該地下水を原位置で浄化し、
前記過酸化水素を、前記地下水中の濃度が0.02%以下になるように導入し、前記ロドコッカス・ジョスティ(Rhodococcus jostii)RHA1株を、前記地下水中の菌数が5.0×108 cells/ml以上になるように導入する、発性有機塩素化合物の浄化方法。
を求める。
Bacteria having the ability to produce catalase and the ability to decompose volatile organochlorine compounds in the presence of oxygen are allowed to act on the volatile organochlorine compounds in the presence of hydrogen peroxide to decompose the volatile organochlorine compounds. Including the decomposition step, the bacterium is a Rhodococcus jostii RHA1 strain, which is a bacterium belonging to the genus Rhodococcus.
The volatile organic chlorine compound is contained in the groundwater, and the groundwater is purified in place to purify it.
The hydrogen peroxide is introduced so that the concentration in the groundwater is 0.02% or less, and the Rhodococcus jostii RHA1 strain is introduced into the groundwater so that the number of bacteria in the groundwater is 5.0 × 108 cells / ml or more. A method of purifying a primary organochlorine compound, which is introduced in the above manner.
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